Biotreatment of Industrial Effluents

| a | gas-liquid interfacial area (gas area per unit liquid volume) |
| BOD | biological oxygen demand |
| C L | liquid phase concentration |
| | liquid phase concentration that is in equilibrium with the gas phase |
| C x | concentration of pollutant at distance x |
| d | bubble diameter |
| d P | particle diameter |
| D i | impeller diameter |
| D T | tank diameter |
| E | activation energy |
| f | recycle ratio |
| J D | Coulburn j factor |
| M A | molecular weight of solute |
| M B | molecular weight of solvent |
| N H | Ammonical nitrogen removed (kg/day) |
| N Pe | Peclet number |
| N Re | Reynolds number |
| N Sc | Schmidt number |
| N T | Total nitrogen removed (kg/day) |
| q o | feed flow rate |
| Q | toxic release rate, g/s |
| R | endogeneous respiration rate (3.9 mg O 2/g MLSS /h) |
| R | Gas constant |
| S | substrate concentration in the exit stream |
| S o | substrate concentration in the exit stream |
| T | temperature |
| U | wind speed, m/s |
| U mf | minimum fluidization velocity |
| V | reactor or aeration tank volume (m 3) |
| V A | molar volume of solute |
| X | cell concentration |
| Y | yield coefficient |
| ? | bed porosity |
| ? g | bubble volume to reactor liquid volume |
| ? | Monod specific growth rate |
| ? B | viscosity of solvent |
| ? max K s | Monod constants |
| ? | Association factor (1-2.6) |
| ? | residence time |
| ? c | sludge age |